EP1244522B1 - Procede et dispositif d'epuration de gaz - Google Patents

Procede et dispositif d'epuration de gaz Download PDF

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Publication number
EP1244522B1
EP1244522B1 EP00978152A EP00978152A EP1244522B1 EP 1244522 B1 EP1244522 B1 EP 1244522B1 EP 00978152 A EP00978152 A EP 00978152A EP 00978152 A EP00978152 A EP 00978152A EP 1244522 B1 EP1244522 B1 EP 1244522B1
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EP
European Patent Office
Prior art keywords
gas
separation discs
rotor
separation
particles
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
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EP00978152A
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German (de)
English (en)
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EP1244522A1 (fr
Inventor
Hans Moberg
Torgny Lagerstedt
Claes Inge
Claes-Göran Carlsson
Stefan Szepessy
Peter Franzen
Leonard Borgström
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Alfa Laval Corporate AB
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Alfa Laval Corporate AB
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Application filed by Alfa Laval Corporate AB filed Critical Alfa Laval Corporate AB
Priority to EP02078688A priority Critical patent/EP1273335B1/fr
Publication of EP1244522A1 publication Critical patent/EP1244522A1/fr
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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B5/00—Other centrifuges
    • B04B5/08—Centrifuges for separating predominantly gaseous mixtures
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01M—LUBRICATING OF MACHINES OR ENGINES IN GENERAL; LUBRICATING INTERNAL COMBUSTION ENGINES; CRANKCASE VENTILATING
    • F01M13/00—Crankcase ventilating or breathing
    • F01M13/04—Crankcase ventilating or breathing having means for purifying air before leaving crankcase, e.g. removing oil
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/12—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
    • B01D45/14—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by rotating vanes, discs, drums or brushes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B5/00—Other centrifuges
    • B04B5/005—Centrifugal separators or filters for fluid circulation systems, e.g. for lubricant oil circulation systems
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B5/00—Other centrifuges
    • B04B5/12—Centrifuges in which rotors other than bowls generate centrifugal effects in stationary containers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
    • B04B—CENTRIFUGES
    • B04B5/00—Other centrifuges
    • B04B5/12—Centrifuges in which rotors other than bowls generate centrifugal effects in stationary containers
    • B04B2005/125—Centrifuges in which rotors other than bowls generate centrifugal effects in stationary containers the rotors comprising separating walls
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01M—LUBRICATING OF MACHINES OR ENGINES IN GENERAL; LUBRICATING INTERNAL COMBUSTION ENGINES; CRANKCASE VENTILATING
    • F01M13/00—Crankcase ventilating or breathing
    • F01M13/04—Crankcase ventilating or breathing having means for purifying air before leaving crankcase, e.g. removing oil
    • F01M2013/0422—Separating oil and gas with a centrifuge device
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S55/00—Gas separation
    • Y10S55/19—Crankcase ventilation

Definitions

  • the present invention relates to a method and an apparatus for cleaning of gas, by means of centrifugal force, from solid or liquid particles suspended in the gas and having a larger density than the gas according to the preamble of claim 1 and claim 7, respectively.
  • the invention is intended for use above all in connection with cleaning of so called crankcase gases, i.e. gases formed in a combustion engine, from particles in the form of oil and/or soot. Alternatively, however, it may be used in other connections.
  • the invention concerns cleaning of gas in a way such that the gas is conducted through a chamber, which is delimited by a stationary housing, and is caused to rotate in the chamber by means of a rotor kept in rotation around a rotational axis, the particles by upcoming centrifugal force being separated from the gas and thrown towards the stationary housing.
  • DE 35 41 204 A1 shows an apparatus of this kind, in which the rotor is formed as a turbine or pump wheel, which is adapted to be brought into rotation by gas to be cleaned entering from below into said chamber.
  • the gas to be cleaned is caused to flow through the turbine or pump wheel from its centre to its periphery, where it leaves the turbine or pump wheel, rotating at the same speed as this wheel.
  • Particles are separated from the gas rotating in the chamber by centrifugal force, and cleaned gas leaves the chamber through an outlet at the upper part thereof. Particles separated from the gas deposit onto the surrounding wall of the chamber, liquid particles coalescing on the surrounding wall and liquid, thereafter, running down it and further out through an outlet situated at the bottom of the chamber.
  • DE 43 11 906 A1 shows a similar apparatus for cleaning of crankcase gases, in which the rotor is adapted to be driven by means of pressurized lubricating oil coming from the combustion engine, the crankcase gases of which are to be cleaned in the apparatus.
  • the driving lubricating oil is supplied to the rotor at its centre and leaves the rotor through tangentially directed outlets situated at a distance from the rotational axis of the rotor.
  • the rotor constitutes in itself, in this case, a device for cleaning of the driving lubricating oil.
  • the cleaned lubricating oil is released in the lower part of the chamber, through which the crankcase gases shall pass in order to be cleaned, and is returned therefrom to the lubricating oil system of the combustion engine.
  • crankcase gases are caused to pass axially through a narrow space delimited in the chamber between the rotor and the surrounding stationary housing. Gas rotating in the space is freed from particles suspended therein, which particles deposit onto the inside of the stationary housing, where liquid particles coalesce and liquid thus formed, thereafter, flows towards an outlet.
  • US-A-2,104,683 describes (with reference to figure 2) that particles in the areas of the radially outermost parts of the separation discs are influenced substantially only by centrifugal forces and move substantially along the generatrices of the separation discs, i.e. in straight paths along radii drawn from the rotational axis of the rotor, whereas particles in the areas of the radially inner parts of the separation discs also and to a very large degree are influenced by flowing gas and, thereby, move in a direction forming an angle with these generatrices.
  • the flowing gas may move substantially freely between the separation discs and may adopt a flow direction determined by among other things the speed by which the gas enters the interspaces between the separation discs and the degree of influence from the rotating separation discs.
  • US-A-3,234,716 describes (with reference to the figures 3 and 4) how particles are separated in the interspaces between conical separation discs. After having got into contact with the insides of the separation discs the separated particles move substantially radially outwardly from the rotational axis of the rotor towards the surrounding edges of the separation discs.
  • the object of the present invention primarily is to accomplish a method of cleaning gases, particularly crankcase gases and an apparatus therefor, which are substantially more effective in separation than the above described technique.
  • the invention provides a method according to claim 1 and an apparatus as defined by claim 7.
  • the improvement hereby obtainable is that particles which have once been separated from the gas have increased possibilities in comparison with use of the previously known technology to remain separated from the gas and, thus, not to be entrained again by gas flowing at a large velocity through the space through which the particles have to pass on their way from the rotor to the surrounding stationary surrounding wall.
  • the particles are collected by means of guiding or conducting members, after which they are conducted further on by means of the centrifugal force towards the surrounding edges of the separation discs while being agglomerated or coalesced to larger particles.
  • the separated particles are then thrown towards the stationary surrounding wall in limited areas distributed along the surrounding edges of the separation discs, whereas between such areas spaces are left for gas flow into or out of the interspaces between the separation discs.
  • the gas to be cleaned may be brought to flow between the separation discs either in a direction from or in a direction towards the rotational axis of the rotor. It is preferred that the flow is taking place in the direction from the rotational axis, as the flow will then be assisted by a pumping effect of the rotor on the gas. Thereby, no auxiliary means are needed to get the gas to flow through the interspaces between the rotating separation discs.
  • the gas to be cleaned preferably is conducted into the interspaces through an inlet space delimited centrally in the stack of separation discs, whereas cleaned gas is conducted out of the interspaces to an outlet space in said chamber, which surrounds the stack of separation discs.
  • an apparatus for cleaning of gas from particles suspended therein comprises a stationary housing that delimits a chamber and that has a gas inlet to the chamber and a gas outlet from the chamber, and a rotor rotatable around a rotational axis and adapted to bring gas to be cleaned into rotation in the chamber.
  • the apparatus according to the invention is characterised in
  • the separation discs may have the form of either complete or frustroms of cones, each separation disc having either one large or several small holes in its central portion for through flow of gas to be cleaned or gas having been cleaned.
  • Such holes in the separation discs form together with the interspaces between the separation discs central parts of one or more inlet or outlet spaces centrally in the stack of separation discs.
  • the flow space centrally in the stack of separation discs communicates with the inlet and that the flow space surrounding the separation discs communicates with the gas outlet, so that gas to be cleaned is caused to flow in a direction from the rotational axis of the rotor through the interspaces between the separation discs.
  • liquid particles depositing on the surfaces of the separation discs will coalesce to larger drops, which when they reach said conducting members and move along these will coalesce to even larger drops.
  • the liquid drops leaving the separation discs are, therefore, substantially larger than the liquid particles contained in the not yet cleaned gas.
  • Even solid particles depositing on the surfaces of the separation discs will accumulate or be agglomerated to substantially larger units, before they are thrown away from the surrounding edges of the separation discs.
  • conducting members of the aforementioned kind are distributed around the rotational axis of the rotor and have an extension such that two adjacent conducting members cross one and the same generatrix of the separation disc at points situated at different distances from the rotational axis of the rotor.
  • the conducting members advantageously are formed such that they can also serve as spacing members between adjacent separation discs. Then, each conducting member along the whole or parts of its extension may bridge the whole distance between two adjacent separation discs. More or less the conducting members will then also determine the flow direction of the gas flowing between the separation discs. None prevents, however, that all or some of the conducting members extend only across part of the axial distance between adjacent separation discs.
  • a conducting member is firmly connected with a separation disc.
  • the stationary housing surrounding the rotor preferably has an outlet at the lower part of the chamber for liquid or sludge having been separated from the contaminated gas and having deposited on the surrounding wall of the chamber.
  • the rotor may be driven by means of any suitable kind of driving device, e.g. an electrically, hydraulically or pneumatically driven motor.
  • FIG. 1 shows a sectional view of an apparatus formed according to the invention and intended for cleaning of a gas from particles suspended therein and having a larger density than the gas.
  • the apparatus includes a stationary housing 1 delimiting a chamber 2.
  • the housing forms a gas inlet 3 to the chamber 2 for gas to be cleaned and a gas outlet 4 from the chamber 2 for cleaned gas.
  • the housing further forms a particle outlet 5 from the chamber 2 for particles having been separated from the gas.
  • the housing 1 includes two parts, which are kept together by means of a number of screws 6. These screws 6 also are adapted to keep the housing fastened to suspension members 7 of an elastic material of some kind, through which the housing may be supported on a support (not shown).
  • a rotor 8 rotatable around a vertical rotational axis R.
  • the rotor 8 includes a vertically extending central spindle 10, which at its upper end is joumalled in the housing 1 through a bearing 11 and a bearing holder 12 and at its lower end is journalled in the housing 1 through a bearing 13 and a bearing holder 14.
  • the bearing holder 14 is situated in the gas inlet 3 of the housing and, therefore, is provided with through holes 15 for incoming gas to be cleaned in the chamber 2.
  • the rotor 8 further includes an upper end wall 16 and a lower end wall 17, which two end walls are connected with the central spindle 10.
  • the lower end wall 17 in a central portion is provided with through holes 18, so that the interior of the rotor may communicate with the gas inlet 3.
  • the lower end wall 17 is provided with an annular flange 19, which is adapted to co-operate with a similar annular flange 20 of the bearing holder 14, so that gas entering through the gas inlet 3 is conducted into the interior of the rotor 8 through the aforementioned holes 18.
  • the flanges 19 and 20 may be adapted to completely seal against each other, but a complete sealing between them is not necessary. The reason for this shall be explained later.
  • the lower end wall 17 is formed in one piece with a hollow column 21 extending axially upwardly from the end wall 17 and sealingly surrounding the central spindle 10.
  • the column extends all the way up to the upper end wall 16.
  • the central spindle 10 is cylindrical, preferably for cost reasons circular cylindrical, and the inside of the column 21 is formed in the same way as the outside of the spindle.
  • the outside of the column 21 has a non-circular cross sectional form, as can be seen from figure 2.
  • a stack of conical separation discs 22 is arranged between the end walls 16 and 17.
  • Each one of the separation discs has a frustoconical portion and in one piece therewith a plane portion 23 closest to the column 21.
  • the plane portion is formed so that it may engage the non-circular column 21 such that the separation disc shall not be able to rotate relative to the column 21.
  • the plane portion 23 is provided with several through holes 24. Irrespective of whether the holes in the various separation discs 22 are aligned axially with each other or not they form together with the interspaces between the central portions of the separation discs 22 a central inlet space 25 within the rotor 8 (see figure 1), which communicates with the gas inlet 3.
  • Figure 2 shows the side of a separation disc 22 facing upwardly in figure 1.
  • this side is called the inside of the separation disc, since it faces in a direction inwardly towards the rotational axis of the rotor.
  • the separation disc on its inside is provided with several elongated ribs 26 forming spacing members between the separation disc and the adjacent separation disc situated above it in the disc stack. Between the adjacent ribs 26 in an interspace between two separation discs flow passages 27 are formed for gas to be cleaned.
  • the ribs 26 extend, as shown in figure 2, along curved paths and form at least at the radially outer surrounding portions of the separation discs an angle with the generatrices of the separation discs.
  • the flow passages 27 for gas to be cleaned extend along paths which are curved in a corresponding way.
  • the ribs 26 extend preferably across substantially the whole of the conical portion of every separation disc and end up in the vicinity of the radially outer surrounding edge of the separation disc.
  • An annular space 28 surrounds the rotor 8 in the housing 1 and forms a part of the chamber 2.
  • the apparatus described above and shown in the drawing operates in the following manner when cleaning gas from particles suspended therein and having a larger density than the gas. It is assumed in this case that the particles are of two kinds, namely partly solids, e.g. soot particles, partly liquid particles, e.g. oil particles.
  • the ribs 26 Owing to the ribs 26 forming an angle with the generatrices of the separation discs the ribs will catch particles moving in contact with the separation discs towards the surrounding edges thereof. The particles caught will be conducted further along the ribs 26 which, thus, will serve as guiding members for the particles.
  • the ribs 26 have a location and an extension such that two adjacent ribs on the same separation disc cross one and the same generatrix of the separation disc at different distances from the rotational axis of the rotor.
  • the ribs 26 distributed around the rotational axis partly overlap each other, if they are seen from the rotational axis.
  • Such overlapping may be to a larger or smaller extent, so that substantially all particles being brought into contact with the inside of the separation disc can be caught by means of curved ribs of this kind and by the ribs be conducted further towards the surrounding edge of the separation disc.
  • the above described function of the curved ribs 26 is obtained independently of the chosen rotational direction for the rotor.
  • the ribs need not necessarily be curved as shown in figure 2. The main thing is that they form an angle with the generatrices of the separation discs and that this angle is such that particles having been caught by the ribs may be guided along these ribs towards the surrounding edges of the separation discs. As to solid particles, the angle of repose of the particles has to be considered in each particular case.
  • the described and shown apparatus has a large separation efficiency and may be produced very cheaply upon a suitable choice of material for the different parts of the apparatus.
  • most of the apparatus parts may be made of plastics.
  • the central spindle 10 should preferably be made of metal.
  • the lower end wall 17 of the rotor and the column 21 may be made in one piece, suitably out of plastics.
  • a part of the rotor formed in this way may form a basis for an automatized mounting of the separation discs 22, which also suitably are made of plastics.
  • the whole rotor mounted in this way, with or without a spindle 10, may form an inexpensive unit for the finished apparatus, which is easily exchangeable.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Centrifugal Separators (AREA)
  • Separating Particles In Gases By Inertia (AREA)
  • Lubrication Details And Ventilation Of Internal Combustion Engines (AREA)
  • Gas Separation By Absorption (AREA)
  • Exhaust Gas After Treatment (AREA)
  • Crystals, And After-Treatments Of Crystals (AREA)
  • Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)

Claims (10)

  1. Procédé pour débarrasser un gaz des particules solides ou liquides suspendues dans ce gaz et dont la densité excède celle du gaz, selon lequel
    - un rotor (8) est maintenu en rotation autour d'un axe de rotation (R) dans une chambre (2) qui est délimitée par une paroi périphérique stationnaire (1) qui l'entoure, ledit rotor comprenant une pile de disques séparateurs coniques (22) disposés coaxialement les uns relativement aux autres, et concentriquement relativement audit axe de rotation, et qui sont pourvus de bords périphériques radialement extérieurs.
    - le gaz à épurer est dirigé, à travers des espaces intercalaires formés entre les disques séparateurs (22), depuis des admissions de gaz jusqu'à des sorties de gaz situées à des distances différentes relativement à l'axe de rotation (R) du rotor, d'où une rotation du gaz avec le rotor et, de ce fait, les particules sont amenées en contact avec l'intérieur des disques séparateurs (22) à cause de la force centrifuge qui s'exerce vers le haut et,
    - dans un premier temps, les particules séparées par la rotation du rotor sont amenées à se déplacer en contact avec les disques séparateurs (22) sur une certaine distance, sensiblement le long des génératrices de ces disques et vers lesdits bords périphériques, puis sont projetées à partir des disques séparateurs vers ladite paroi périphérique (1).

    caractérisé en ce que
    - les particules séparées qui se déplacent en contact avec les disques séparateurs (22) sensiblement le long des génératrices de ceux-ci sont attrapées et dirigées, avec les particules attrapées de manière semblable, plus avant vers lesdits bords périphériques des disques séparateurs, le long de parcours qui forment un angle avec lesdites génératrices et
    - en ce que les particules séparées sont sensiblement forcées à quitter lesdits parcours et à être projetées, depuis les disques séparateurs (22), uniquement dans des zones limitées situées à une certaine distance les unes des autres le long des bords périphériques des disques séparateurs respectifs.
  2. Procédé selon la revendication 1, selon lequel le gaz à épurer est dirigé entre les disques séparateurs (22) dans une direction qui va depuis l'axe de rotation (R) vers lesdits bords périphériques des disques séparateurs.
  3. Procédé selon la revendication 2, selon lequel le gaz à épurer est dirigé dans un espace d'admission central (25) dans la pile de disques séparateurs (22) et, à partir de ce point, traverse les espaces intercalaires compris entre les disques séparateurs (22), après quoi le gaz propre est dirigé hors de la chambre (2) à travers une sortie de gaz (4) qui communique avec un espace de sortie (28) qui est formé par et entre la pile de disques séparateurs (22) et la paroi périphérique stationnaire (1).
  4. Procédé selon l'une quelconque des revendications précédentes, selon lequel le gaz à épurer est entraîné dans la rotation du rotor tout en passant à travers les espaces intercalaires compris entre les disques séparateurs (22) au moyen d'éléments (26) qui pontent les espaces intercalaires compris entre des disques séparateurs adjacents.
  5. Procédé selon l'une quelconque des revendications précédentes, selon lequel le gaz est dirigé entre les disques séparateurs (22) le long de parcours (27) sensiblement parallèles auxdits parcours prévus pour les particules séparées.
  6. Procédé d'épuration de gaz de carter provenant d'un moteur à combustion selon l'une quelconque des revendications précédentes.
  7. Dispositif pour débarrasser un gaz de particules solides ou liquides suspendues dans ce gaz et dont la densité excède celle du gaz, ledit dispositif comprenant un logement stationnaire (1) qui délimite une chambre (2) et est pourvu d'une admission de gaz (3) dans la chambre et d'une sortie de gaz (4) hors de la chambre, et d'un rotor (8) qui peut tourner autour d'un axe de rotation (R) et qui est adapté pour l'épuration du gaz en rotation dans la chambre (2), dispositif dans lequel
    - le rotor (8) comprend une pile de disques séparateurs coniques (22) disposés coaxialement les uns relativement aux autres et concentriquement relativement à l'axe de rotation (R) du rotor, lesdits disques séparateurs délimitant entre eux des espaces intercalaires qui rendent possible le passage ininterrompu du gaz,
    - au moins un premier espace d'écoulement de gaz (25) est delimité centralement dans la pile de disques séparateurs (22) et communique avec des parties radialement intérieures des espaces intercalaires compris entre les disques séparateurs (22),
    - au moins un second espace d'écoulement de gaz (28) est délimité par et entre la pile de disques séparateurs (22) et le logement stationnaire (1) et communique avec des parties radialement extérieures des espaces intercalaires compris entre les disques séparateurs (22), et
    - lesdits premier espace d'écoulement de gaz (25) et second espace d'écoulement de gaz (28) communiquent respectivement avec l'une et l'autre desdites admissions de gaz (3) et sortie de gaz (4), le dispositif étant d'autre part formé de sorte à conduire sensiblement, à travers les espaces intercalaires compris entre les disques séparateurs, la totalité du gaz fourni à ladite chambre (2) par l'intermédiaire de l'admission de gaz.

    caractérisé en ce que
    chacun des disques séparateurs coniques (22) est en contact ou est connecté, sur sa partie intérieure, avec des éléments de guidage allongés (26) mutuellement séparés par une certaine distance, chacun d'eux s'étendant en formant un angle avec les génératrices des disques séparateurs (22), depuis un point situé à une première distance de l'axe de rotation (R) du rotor jusqu'à un point situé à une seconde distance plus grande de l'axe de rotation (R) du rotor, lesdits éléments de guidage (26) pour chaque disque séparateur (22) se terminant au voisinage du bord périphérique du disque séparateur et espacés les uns des autres comme illustré le long du bord périphérique.
  8. Dispositif selon la revendication 7, dans lequel lesdits éléments de guidage (26) sont répartis autour de l'axe de rotation du rotor et sont pourvus d'une rallonge, de sorte que deux éléments de guidage (26) adjacents traversent une même génératrice du disque séparateur en question en des points situés à des distances différentes de l'axe de rotation (R) du rotor.
  9. Dispositif selon la revendication 7 ou 8, dans lequel les éléments de guidage (26) pontent les espaces compris entre des disques séparateurs (22) adjacents.
  10. Dispositif selon l'une quelconque des revendications 7 à 9, dans lequel ledit premier espace d'écoulement de gaz (25) communique avec l'admission de gaz (3) et ledit autre espace d'écoulement de gaz (28) communique avec la sortie de gaz (4).
EP00978152A 1999-11-15 2000-10-27 Procede et dispositif d'epuration de gaz Expired - Lifetime EP1244522B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP02078688A EP1273335B1 (fr) 1999-11-15 2000-10-27 Procédé et dispositif d'épuration des gaz du carter de vilebrenquin

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
SE9904116A SE515302C2 (sv) 1999-11-15 1999-11-15 Ett sätt och en apparat för rening av gas
SE9904116 1999-11-15
PCT/SE2000/002120 WO2001036103A1 (fr) 1999-11-15 2000-10-27 Procede et dispositif d'epuration de gaz

Related Child Applications (1)

Application Number Title Priority Date Filing Date
EP02078688A Division EP1273335B1 (fr) 1999-11-15 2000-10-27 Procédé et dispositif d'épuration des gaz du carter de vilebrenquin

Publications (2)

Publication Number Publication Date
EP1244522A1 EP1244522A1 (fr) 2002-10-02
EP1244522B1 true EP1244522B1 (fr) 2006-02-15

Family

ID=20417713

Family Applications (2)

Application Number Title Priority Date Filing Date
EP02078688A Revoked EP1273335B1 (fr) 1999-11-15 2000-10-27 Procédé et dispositif d'épuration des gaz du carter de vilebrenquin
EP00978152A Expired - Lifetime EP1244522B1 (fr) 1999-11-15 2000-10-27 Procede et dispositif d'epuration de gaz

Family Applications Before (1)

Application Number Title Priority Date Filing Date
EP02078688A Revoked EP1273335B1 (fr) 1999-11-15 2000-10-27 Procédé et dispositif d'épuration des gaz du carter de vilebrenquin

Country Status (14)

Country Link
US (1) US6821319B1 (fr)
EP (2) EP1273335B1 (fr)
JP (2) JP4699668B2 (fr)
KR (2) KR100596121B1 (fr)
CN (2) CN1131730C (fr)
AT (2) ATE303861T1 (fr)
AU (1) AU1563801A (fr)
BR (2) BR0017409B1 (fr)
CA (1) CA2390944C (fr)
DE (2) DE60026060D1 (fr)
NO (2) NO321660B1 (fr)
PL (2) PL194816B1 (fr)
SE (1) SE515302C2 (fr)
WO (1) WO2001036103A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
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CA2390944A1 (fr) 2001-05-25
EP1273335A3 (fr) 2003-04-02
KR100596120B1 (ko) 2006-07-19
EP1273335A2 (fr) 2003-01-08
ATE317728T1 (de) 2006-03-15
SE9904116D0 (sv) 1999-11-15
JP2003513792A (ja) 2003-04-15
JP2005042698A (ja) 2005-02-17
CN1280526C (zh) 2006-10-18
NO20022283D0 (no) 2002-05-14
BR0017409B1 (pt) 2008-11-18
DE60022555T2 (de) 2006-01-19
NO321660B1 (no) 2006-06-19
PL202029B1 (pl) 2009-05-29
BR0015559A (pt) 2002-07-09
ATE303861T1 (de) 2005-09-15
JP5314826B2 (ja) 2013-10-16
US6821319B1 (en) 2004-11-23
SE9904116L (sv) 2001-05-16
KR20020053081A (ko) 2002-07-04
KR100596121B1 (ko) 2006-07-19
AU1563801A (en) 2001-05-30
NO20025068L (no) 2002-07-15
EP1273335B1 (fr) 2005-09-07
SE515302C2 (sv) 2001-07-09
JP4699668B2 (ja) 2011-06-15
CN1131730C (zh) 2003-12-24
CN1390158A (zh) 2003-01-08
WO2001036103A1 (fr) 2001-05-25
NO20022283L (no) 2002-07-15
NO20025068D0 (no) 2002-10-22
EP1244522A1 (fr) 2002-10-02
DE60022555D1 (de) 2005-10-13
PL194816B1 (pl) 2007-07-31
CA2390944C (fr) 2008-06-03
CN1515789A (zh) 2004-07-28
DE60026060D1 (de) 2006-04-20
PL355419A1 (en) 2004-04-19
NO332890B1 (no) 2013-01-28

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